Apparatus for extracting volatile oils froh solid substances



2 KQZQL 1,589,838 MCGARVEY cuNE APPARATUS FOR EXTRACTING VOLATILE GIL-3 FROM SOLID SUBSTANCES T Jame Filed August 24, 1925 4. Sheets-Sh e'ef; l

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June 22 9 19221 M Gi-ERVEY QMME KTHACTIHG VOLATILE om mom sow) SUBSTANCES APPARATUS FOR 13 Sheets=5heeia Filed August 24, 1923 June 22 1926. 1 55383 MGGARVEY cLmE APPARATUS FOR Eli TRACTING VOLATILE OILS FROM SOLID SUBSTANCES 4 Sheets-Sheet 5 August 24, 192

Jame 22 192$ M GARVEY CLEME APPARATUS FOR EXTRACTING VOLATILE OILS FROIZ SOLID SUBSTAEICES Filed August 1923 4 Sheets-Sheet Gama 5 5 nvanlfir J 5cm; 4% P I In This invention relates to an apparatus for extracting volatile oils from solid substances by steom distillation, and has been designed more particularly to edect the extraction o? turpentine? from comminuied wood in. the form or sawdust, pulp and chips; such com- .minuted Wood representing the Waste product of lumber mills. which is ordinarily utilized as fuel to furnish the power required by the mill.

Heretofore, where the extraction of valuable material from the Waste before burnin the letter has been practiced, it has been cusiomory to load the Waste into retorts wherein the oil is extracted by the direct action oi steam thereon, and then transfer the Waste from the retort to the power plant of the mill fi'eqncntly located at some distonce "from 'the'lct ter. This method of handling is intermittent, the retort being filled, sealed, operated, opened, and emptied; involving conniderable expense for labor; end one or the objects of the present invention is to provide a retort for the extraction oi the oil which may conveniently constitute c section or link of a continuously operating conveyor from the mill to the power plant or other point Where the waste is burned or otherwise disposed of. Another object of the invention is to provide an apparatus for the extraction of volatile oil from the waste Wood wherein the heating agent (preferably steam) may be most ei'iiciently and economically used for the heating of the material to the required extent to vole-- tilize the oil. another object, ancillary 'lo the above, is to provide a means of heating by which the beat shall be most intimately, thoroughly end uniformly applied to 'lhe entire mass of the material. Another object, is to provide a means of beating; the material undergoingtreatment which will deliver the heat units necessary to vaporize the oil in the chips without having steam condense on. and thus increase the moisture content of, the latter, which decreases its value as fuel. on improved uro'paratus wherein the heat is mainly supplied by high pressure steam out of direct contact with the material treated. ind wherein the latter is also subjected to. the direct action of low pressure, oil "Free steam in such a quantity and so circulale'd thercthrough that no portion of said steam can ever become saturated with oil vapor, which would retard or arrest the furealisation one AFAgFiBiJ cc,

Another object is to provide Lil-89338 their vaporization of the letter; thereby increasing the rate of evaporation of the oil. lr further important object of the invention is to provide on of the character specified of such a construction that the some may, with e. minimum of trouble, he disassembled to the necessery extent for in SPEIC'EIOR, cleaning and regcirs when re- -.nined. A inrther object 1s to provide an apparatus including," e plurality of superposed challnbe e cbrongh which the mcleriel passes succe rely from top bottom'and in each of which it is so and caused to travel; over the surface of 2 hot late and wherein the low pressure steam in direct contact with the material. is coused to travel countercurrent to the blow of the material through and around the axis of each of the successive chambere, whereby the meberial is thoroughly end evenly subjected to the action of the s em. I

Gtber objects and cttendent advantages of the invention will be apparent to persons skilled in the art from the following deteil description taken in connection with the occompanying; drawings in which I have illustraced one practical and workable embodiment of the principle 0'? the invention and wherein. 3

l is 2. view partly in elevation and motif} in vertical secfzion of my improved apparatus;

Fig. 2 is a top plan view of some, imrtly broken out;

Fig? is a top plan View of one of the ennulor meeting plates, -with the drum and shell in horizontal section;

-Fig. i is an edge elevation of the heating plate shown in Fig. 3;

Fig. 5 is s top plenview of one of the scrapers which revolves over the surface of e beating plate. with the drum and shell in horizontal section;

Fig. 6 is a top plan view on a reduced scale of a heater for the hot plate shown in Figs. 3 and 4 that directly underlies and carries the letter;

Fig. 7 is a side elevation, partly in section of the heater shown in Fig. 6;

Figs. 8 and 9 are detail views in top plan and side elevation, respectively, of one of scraper arms-end tne manner and menns of mounting the so me on the angle iron ring of the scraper;

18 is an enlarged elevation showing one of series of radial openings or band holes in the cylindrical shell through which access is had to the scrapers and their supporting and adjusting devices, with the cover of the o ening removed;

Fig. 11 is a orizontal section on the line 11-11 of Fig. 10;

Fig. 12 is a vertical section on the line 1212 of Fig. 10; and

Fig. 13 is a horizontal section on the centrally offset line 13-13 of Fig. 1, with the lower cover plate of the drum removed.

Referring to the drawings, 15 designates a hollow casting supported on four radial piers 16 and forming the lower or base member of a central sectional stationary steam chamber or drum. In the lower end of the casting 15 is a large opening 17 normally closed by an internal cap or cover plate 18. In the side of the member 15 is an opening 19 through which high pressure or superheated steam is supplied through a supply pipe 20, and near the bottom of the same is another opening 21 through which water of condensation is discharged through a pipe 22. superposed on the base member 15 isa series of annular sections 23, one of which is shown in isolated detail in Figs. 6 and 7, each provided with internal top and bottom flanges 24 and 25 by which they are rigidly united by bolts 26. Superposed on the topmost section 23 is a hollow casting 27 having a large opening 28 in its upper end normally closed by a cap or cover plate 29.

The parts thus far described constitute a hollow heating, drum of sufficient diameter to permit a workman to enter the same through the upper opening 28.

Figs. 6 and 7 show in detail tl'e structure of one of the drum sections 23, from which it. will be observed that the central annular member is provided with two (upper and lower) groups of hollow radially disposed tubes 30 that are closed at their outer ends and at their inner ends communicate freely with the interior of the annular section 23. It will further be observed that at one point in each series a tube is omitted leaving a s ace designated by 31 in Fig. 6; and it will a so be observed by reference to Fig. 7 that the space 31 in the lower series of tubes is laterally offset bythe width of a pair of tubes from the corresponding space of the upper series; the purpose of which will be hereinafter disclosed.

Resting upon each horizontal group of heating tubes 30 and encircling and snugly fitting the central section 23 is the annular heating plate shown in detail in Figs. 3 and 4 and designated as an entirety by 32. This a thin metal plate com-'eniently made in a plurality of sectors 32' having depending "flanges 32' at their ends bolted together.

opening 33 therein, the edges of which are, however, joined by a narrow oblique bridge 34, the upper surface of which is flush with the top surface of the plate, and the purpose of which will presently appear. The opening 33 of the plate registers with the s ace 31 in the underlying tubes. The depen ing radial flanges 32'? of the plate are so spaced that each will lie alongside one of the heater tubes or arms 30, whereby the latter act as stops to prevent any turning movement of the plate under the drag of the material advanced by the scraper arms thereover as hereinafter described.

On the outer surface of the top member 27 of the central steam drum is a horizontal flange 35 on which is supported the hub 36 of a circular cover plate 37 that constitutes the top closure of the annular distilling chamber surrounding the central steam drum.

Surrounding and enclosing the arts thus far described is ,a cylindrical shel 38 con venieutly made of thin metal and strengthened by top and bottom angle rings 39 and 40. Attached to the lower side of the lower angle ring 40 is a ring gear 41 engaged by a pinion 42 on a shaft 43 for driving the same and thus rotating the shell 38. On the lower side of the gear 41 is formed a V- shaped annular track 44 that travels on grooved rollers 45 mounted on horizontal stub shafts 46 supported by the supporting piers 16 ofthe steam drum.

At points in the shell 38 correspondingto the levels of the several heating plates are formed radial openings or hand holes 47; four such openings being shown, ninety de grees apart, at the level of each heating plate, and each opening being surrounded by a short circular flange 48 eqnipped'with a removable cap or cover 49.

Describing now the circular scrapers, of which one is provided for each of the heating plates, 50 designates an angle ring of an outside diameter slightly 'less than the internal diameter of the shell 38. As shown in Fig. 12, the horizontal limb of the angle ring 50 overlies the outer peripheral portion of the heating plate 32. As shown m Fig. 11 the vertical limb of the ring 50 is vertically slotted at uniform intervals, as shown at 51, to accommodate the outer end portion of the radial scraper blades 52; the lower edge of each of the latter being cut away, as shown at 53 in Fig. 9, so that the lower edge of the blade lying within the ring 50 may be substantially flush with the lower surfac qf the ring, the inner end of the cut awayportion being beveled, as shown at 54, to provide ample clearance from the trots 55, one of which connected by cop with g lotto? being icoseiy limit-eat 'Llbe eoci sficlczi, cbcwo et 52 to jamming tbs mctcriai bec: and the o iews 110, 11 and iilcstmtc the menses of SEEE' JUFibig t if) scoops; ring 50 co :bom tbs rcvoiviiig At icowob; oincty [icg'rccs 225mm; on the lioi'izcotcl limb to ring bra-bosons poir of adjacent blcclcz's o bio-ck 5S with 23 pair of boics 59 with holes 3% in the T coco ing a woii 4: the s ieii 38 l, ilQtl- :aontol iowcr on Wbicb recto plot-c 53 tbet projects iowoidly abe /c block 58 sod is ocgooretoo from the letter by s group of spacing sachets This $2 is opertcsctl in line with-the epcrtui'cs 59 cm? through the some are pacsczi e coir: of cop screws cc tbrccding into the holes 59 and t}, (in the mites eclo'c of the plate $2, out

e m inc of openiiig H, is o ties-ending a. pen" of ecijusting screws nst the Wall underlying '5 the opcciog ii; the esscmbly time to both cents? coil subject-t the ring on on 1 from the wail of sbcll and out oi yisictionei con- 35 with the booting piste, with capacity the Mod s swoop over cod follow the surfocc of beating plot/e V By microbes to Fig. 12, it will be scco that the aegis rizigs 59 also serve to scei the openings between the cdgcs of he heating omit revolving shell, so that cii'cuistiog is will not mse between the plate edges cacti tbs revolving; shell, this scaling rcsulting from the foot that the sci-er spaces between the shell and; the vertical flange of ring o0 become fille i with the matci'iei being; treated, iil'iill since the ring and sbeli z'evoive together, this packing material does not produce friction 01 have 59 any tendency to jam between relatively sliding surfaces.

An important advantage of the abovedcsci'iberi construction lies in the fact that by disconnecting the overhead tube connections, clcscribecl below, and removing the plates 62 through the band boics the shell can be strippeii enclwise from the enclosed plates, scrapers and drum for inspection, cleaning and reg/127's when required.

Describing the means for feeding the material to be treated into the upper end of the annular clistilling chamber, 67

designates a neck formed on the cover plate 33, on which is mounted a tubular section (53 closcci at its uppci end by a cap plate and having a short iaterci bmncb 'Ill to which is connected 9, shoib length of feed tube "Z1. To t-bc outer end cf tbe tube 73. is connected smother fecd tube section 72 having on its upper siaie an opcnin c 72 surmounted by a hopper 1 3' through woich tbc material may be deiivcred from the dis-- cbci'gc cud of a conveyor (not shown) or otherwise. Within the tube TF2 is e plunger '54 connect cot to and fcciprocat/emi by e piston 75 in o stcam or otlici' cylinder 76 connected to the outer eliti fl f the tube 72. As the material is fed through the boppci T 3 and opening; T3 into the tube M it is, at each foiwvoid movement of the plunges, 643m end aaivsnccti to the tubular section 71 tiro opiicg thence through upright section 58 aooi ncci f5? onto tbc toloioost booting pictc.

From the lowermost booting pietc we metciciai is discharged c, boo' ser T? mounted in and cxtcnding tbroii mailer plate 78 that is attached to s. homzontal flcogc 15 on the outer cylindrical wail of the base member 15 of the steam drum or com, said bopgoer resting upon the upper scige of at discharge opcning it formed in the upper side of a discharge tube sec tion 80; ibis latte! beiog' cquippcfi with a plunger 81 actuated by c, piston 82 in' a steam or other cylinder 83 connected to one end of the tubular section $0. To the opposits end of the latter is connected another tubular discharge section 8'; through which the, material is advanced by successive strokes of the piuogct' 31 to any desired point of delivery, in some cases to o, convcyoi: (not shown) which carries tbc metcrial. to the place Where it is to be burnedor fuittber treat-ed for the extraction of i'csin or other valuable substances contained therein.

Steam is admitted to the bottom of the annular clistillino chamber by any suitable means, such as pips 85 heroin shown as extending through one side of the discharge hopper 77, which latter be provided with a hand hole 86 equipped with a cover plate 87 for access t-bcreto in case of any clogging of the mot'ctiei.

v The annular distilling chamber is cfiectively sealed at the bottom by means of an annular wall formcoi between a pair of stationary outer and inner concentric rings 88 and 89 joined at their lower ends by e horizontol annular plate 90, enoi a rotating ting 91 attached to and depending from the lower end of the cylindrical sbcli and extending nearly to the bottom of the Well; the latter being portl filled with any suitable s oling' liquid. The annular well or t1 011fl is supported from the piers 16 and to its inner Wall may be attached the outerpcripber of the annular plate 78. A similar seal is ployed at the upper end of the annular l the .wells and constitute dust covers for rings 91 and 93 are formed on their upper edges with horizontal flanges which cover seals to prevent the material being handled from accumulating in the seal wells.

In order to effect a thorough, intimate and uniform contact of the steam admitted through pipe 85 (which expands to approximately atmospheric pressure in the' distilling chamber) with the material treated, 'I provide means whereby this steam for the most part is caused to follow the entire path of travel of the material and preferably in the reverse direction. I have already stated that the successive heating plates from top to bottom are provided with openings to drop the material from one plate onto the next, which openings are laterally offset or staggered relatively to each other around the axis of the distilling chamber in a direction reverse to the direction of travel of the scrapers. Normally the steam in flowing upwardly would seek a direct path from the opening of each plate to the relatively offset opening of the next higher plate, and would not flow around and through each individual compartment between adjacent plates. I have, however, provided means whereby the bulk of the steam is caused to travel around and through each individual compartment before passing upwardly into the next higher compartment; and this means, as best shown in Fig. 7, comprises a pair of swinging bafiie plates 94 that are suspended from a pair of adjacent heating tubes 30 lying next to the discharge opening 33 of the heating pla" and the registering opening 31 of the tubular heating device; these baflle plates extending down to approximately the top surface of the next underlying heating plate. These bafiles practically close the short passageway from a lower opening to the next higher opening,

and cause the steam to take the long pas-- sage around the drum section 23 before it can pass upwardly through the higher opening. As the scraper arms, after passing over the openings 33 through which the material is dropped strike the lower ends of the bailies 9-1, the latter are swung upwardly just 'sutliciently to permit the blades to pass therebeneath; but when the bafiles are opened to that extent the gap between their lower edges and the heating plate is practically closed by the blades themselves, so that little or no steam finds its way upwardly by the short path. Manifestly a single baffle plate would be fairly eiiicientto serve this function, but I prefer'to employ a pair of such baflle platesbpening successively as affording a more perfect seal for confining the flow of the steam to the long circuitous path. It is also evident that the direction of flow of this steam may be reversed, so as to be parallel instead of counter-current. 1

To carry off the vapor distilled I provide a discharge pipe '95 that is connected into the upper portion of the tubular feed section 68 and is equipped with a controlling valve 96. For the purposes of more or less preheating the material and condensing out some of the water vapor, I preferably provide means for directing the flow of the distillate more or less through the inflowing material before it passes into the discharge line 95; the same-comprising a laterally extending pipe 97 communicating with the pipe 95 an equipped with spaced branches 98 and 99 connecting into the feed section 71 and equipped with controlling valves 100 and 101 respectively. Manifestly, by closing the valve 96 and opening either of the valves 100 and 101, theifiow of the distillate may be dire'eted more or less through the incomin material giving up a part of its heat an water vapor to the latter. The advantage of this is not only or mainly that it prehe'ats the material, but it" condenses out the surplus steam in the mixture, reducing the latter to a turpentine saturated condition, and thus increasing the ratioof turpentine to water vapor in the mixture that goes to th condenser.

' It is believed that the structural features and mode of operation of my improved a paratus will be clear from the foregor wi e scription without further elaboration, ut I desire to briefly point out some of the more important novel features of treatment and the advantageous results flowing therefrom. The indirect heating of the material by the latent heat of high pressure or superheated steam transmitted through the heating plates has the function and effect of vaporizing and driving off the turpentine contained in the material without saturating the material with moisture which is, of course, a detriment to its subsequent fuel value. The radial heating tubes are employed mainly to increase the heating surface over what would be obtained by using a simple steam drum withoutsuch tubes. On the other hand, by subjecting the material treated to direct contact with low pres-f menses s mg the role of evaporation of the turpentine from the material, and is also available for preheating the material, by which the ratio of the turpentine to the Wet/er vapor in the mixture that use to the condenser for final separation is inc-reused. This beneficial efiect ofthe low pressure steam in direct 'contact with the material is manifestly enhanced by causing the steam to flow countercurrent to the travel of the solid materiel throughout the entire path of the lettewend simnltzineously maintaining the solidinste riel in a constant state of agitation and tumbling, whereb practically every particle of the letter is subjected to the action of the steam,

In situations where excessive wetting of the-material is not objectionable, as where it is not subsequently used for fuel, thev indirect lleatin herein shown and described may be omitte and steam admitted into direct and intimate contact with the material in suiticient volume to both volatilize the oil and maintain a circulation of the vapor in a. nonsatursted condition;

It is manifest that the physical embodiment of the invention herein described and illustrated may be widely varied in details Without departing from the principles involved or sacrificing any of the advantages secured. Hence I reserve all such variations and modifications as fall within the spirit and purview of the appended claims.

I claim-- 1. In a retort for distilling oil from solid substances, the combination of a series of spaced superposed stationary plates,s rotutable shell surrounding said plates, scrapers resting on said lat/es and connected to and adapted to be driven by said shell, means for admitting the material to he treated onto the top plate of the series, means for passing the material from each plate to the next underlying plate, means for heating the material, and means for discharging the mate rial from the lower end of the retort.

21 in a retort for distilling oil from solid substances, the combination of a series of spaced superposed stationery plates, a rotatnble shell surrounding said plates, scrapers resting on said plates and connected to and adapted to be driven by said shell, means,

for admitting the material to be treated onto the top plate of the series, menus for passing the material from each plate to the next underlying plate, means for admitting a. heating medium to the spaces between adjacent plates, and means for discharging the material fl'OIll tl13 lower cud of the retort.

3. in a retort for distilling oil from solid substances, the combination of a central up right column, 11 series of vertically spaced annular plates 'encircling and supported from said column, a rotute'oie shell enclosing said column and plates, scraper blades resting on said pistes and connected to and adopted to be driven by said shell, means for sdinitting the materiel to he treated onto the top plate of the series, means ior fllill ing the material from each plate to the next resting on plates and connected to end adopted in be driven by said shell, stationary top and bottom cover plates for sold shell, means for feeding material to be treated through said top cover plate onto the topmost stationery plate, menus for delivering the material from each plate to the nest on derlying plate, means for'admi'tting a fluid heating medium into said shell, means for Sealing the ends of said shell sneinsl; escape of said heating medium, and means for discharging the meteriul through said bottom cover plate. 1

5. in e retort for distilling oil from solid substances, the combination ole central upright column, a. series of vertically speoed annular plates encircling end supported from said column, a. rotatable shellenclosing' said column end plates, top and bottom cover plates for said shell mounted on the upper and lower ends of said column, scrapers resting on said annular pistes and connected to and adapted to be driven by said shell, means for feeding material to be treated through said top cover plate onto the topmost annular piste, means for delivering the material from each plate to the next underlying plate, means for admitting s. fluid heating medium into ssid shell, means for sealing the ends of said shell and said top and bottom cover plates, and means for discharging the material through said bottom llil said drum, means for heating said plates by said steam, a rotatable shell surrounding said pistes, scrapers resting on said isles and connected to and adopted to he rivcn by said shell, means for admitting the meterial lo be treated. onto the top plate of the series, means for psssing the material from each plate to the next underlying plate, and means for discharging the material from the lower end of the retort.

T. In a retort for distilling oil from solid substances, the combination of e stationery upright; steeni e series of spaced cally groups of radial tubes closed at their outer ends and at their inner ends connected into and communicating with said drum, annular plates encircling said drum and resting on said tubes, means for supplying steam to said drum, a rotatable shell encircling said plates, scrapers resting on said plates and connected to and adapted to be driven by said shell, means for admitting the material to be treated onto the top plate, means-for delivering the material from said plate to the next underlying late, and means for discharging the material from the lower end of the retort."

8. In an apparatus of the character described, the combination of a series of vertically spaced stationary circular plates formed with openings that are-relatively ottset l'aterally around the centers of said plates, a rotatable shell encircling said plates, scraper blades resting on sald lates and connected to and adapted to be riven by said shell, means for admitting a heating 'fluid to one end of said shell, and means for causing said fluid to flow through each compartment between ad'acent plates around the axis thereof before owing into an adjacent compartment.

9; In an apparatus of the character described, the combination of a series ofvertispaced stationary circular plates formed with sector-shaped openings that are relatively offset laterally around the centers of said plates, a rotatable shell encircling said plates, radially disposed scraper blades resting on said plates and connected to and adapted to be driven by said shell, means for admitting a heating fluid to one end of said shell, and swin ing bafile plates suspended from correspon ing edges of said openings and each extending downwardly substantially to the top of the next underlyin plate; said bafile plates serving to compe said heating fluid to follow a circuitous path around the axis of each compartment between adjacent circular plates before flowing into an adjacent compartment.

10. In an apparatus if the character described, the combination of a stationary plate,'a rotatable shell encircling said plate,

a scraper ring mounted on and within said shell, and a series of scraper arms resting on said plate and at their outer ends hinged to said scraper ring.

11. In an apparatus of the character described, the combination of a stationary circular plate, a rotatable shell encircling said plate, a scra er ring mounted on and within said shell a jacent to the periphery of said plate, and a series of radially disposed scraper arms resting on said plate and at' their outer ends hinged to said scraper ring.

12. In an apparatus of the character described, the combination of a stationary circular plate, arotatable shell encircling said plate and provided with a series of hand holes spaced around. its circumference, a scraper ri'ng Within said shell, means for adjustably supporting said ring on the bottom edges of said hand holes, a series of radially disposed scraper arms resting on said plate to said shell permitting the latter to be bodily withdrawn endwise from said core and plates.

14. In an apparatus of the character described, the combination of a central upright core member, a series of vertically spaced annular plates encircling and supported on said core member, a shell encircling said plates, scraper rings within said shell adjacent to the peripheries of said plates, radially disposed scraper blades resting on said plates and at their outer ends pivoted to said rings,

means for detachably connecting said rings to said shell permitting the latter to; be bodily withdrawn endwise from said core and plates, acircular trackway on which the lower end of said shell is rotatably mounted and means for turning said shell on said trackway. I

15. In a distilling retort of the character described, the combination of a stationary steam drum, a series of spaced annular plates surrounding said drum, a single shell enclosing said drum and plates, scrapers on said plates adapted to be driven by said shell, gearing for rotating said shell, and means for feeding solid material to, and discharging it from, said shell.

16. In a retort for distilling oil from solid substances, the combination of a stationary upright steam drum, a series of spaced groups of radial tubes connected at their intr ends into and communicating with said drum, annular plates encircling said drum and resting on said tubes, a rotatable shell 17. In a distilling retort of the character described, the combination of a stationary upright steam drum, a series of spaced annular plates surrounding said drum, a rotatable shell encircling said drum and plates, scrapers on said plates adapted to be driven by said shell, stationary top and bottom cov- #31 plates for said shell carried by said drum,

means far creating liquid seals between the) ends 01? said shall and said jzop and betmm. cover plates, and dust covers for said s saling meam.

18. in a retaz't far disiilling ail from solid substanaes, the combination of a stationary steam drum a series of spaced annular haacing plsltes smmunding said drum, a rotatable plates, scmpsm w driven by said shell, means for efiecsing the travel of the malaria heated 0W3! said plates, means Or fading the material 00 and discharging it from saicl shell, and driving mechanism for w said. shell, and said feeding and (lischarging mean-a losated enti rely outside: said retort.

McG-ARVEY CLINE 

